Datasets
-
Temperature, K x Pressure, kPa x Mole fraction (8)
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Water (3) - Liquid |
Mole fraction of Diethyl carbonate (1) - Liquid |
Mole fraction of Diethyl carbonate (1) - Gas |
Mole fraction of Water (3) - Gas |
353.15 |
61.78 |
0.0469 |
0.9037 |
0.3572 |
0.4134 |
353.15 |
94.30 |
0.0484 |
0.5032 |
0.1633 |
0.1379 |
353.15 |
109.49 |
0.0488 |
0.0491 |
0.0318 |
0.0757 |
353.15 |
93.14 |
0.0976 |
0.6531 |
0.2068 |
0.3065 |
353.15 |
103.76 |
0.0989 |
0.2994 |
0.1180 |
0.1688 |
353.15 |
108.91 |
0.1179 |
0.1521 |
0.0755 |
0.1626 |
353.15 |
103.54 |
0.2056 |
0.3962 |
0.1465 |
0.3367 |
353.15 |
94.72 |
0.2183 |
0.6704 |
0.2198 |
0.5470 |
353.15 |
100.45 |
0.2481 |
0.5005 |
0.1756 |
0.4440 |
353.15 |
107.16 |
0.2518 |
0.2491 |
0.1132 |
0.3160 |
353.15 |
112.94 |
0.3095 |
0.0489 |
0.0394 |
0.2750 |
353.15 |
109.89 |
0.3981 |
0.0986 |
0.0757 |
0.3531 |
353.15 |
101.47 |
0.4010 |
0.3021 |
0.1507 |
0.4540 |
353.15 |
104.76 |
0.5022 |
0.1504 |
0.1175 |
0.4249 |
353.15 |
106.01 |
0.5052 |
0.1250 |
0.1038 |
0.4193 |
353.15 |
105.10 |
0.7015 |
0.0295 |
0.0718 |
0.4366 |
363.15 |
87.85 |
0.0465 |
0.9058 |
0.3710 |
0.4040 |
363.15 |
134.63 |
0.0483 |
0.5042 |
0.1880 |
0.1250 |
363.15 |
156.65 |
0.0491 |
0.0492 |
0.0350 |
0.0730 |
363.15 |
131.90 |
0.0973 |
0.6537 |
0.2200 |
0.2990 |
363.15 |
147.90 |
0.1012 |
0.2983 |
0.1340 |
0.1820 |
363.15 |
155.27 |
0.1190 |
0.1460 |
0.0840 |
0.1520 |
363.15 |
147.72 |
0.2019 |
0.3928 |
0.1660 |
0.3110 |
363.15 |
134.19 |
0.2122 |
0.6756 |
0.2340 |
0.5300 |
363.15 |
143.65 |
0.2471 |
0.5006 |
0.2060 |
0.4200 |
363.15 |
152.97 |
0.2508 |
0.2490 |
0.1320 |
0.3030 |
363.15 |
160.62 |
0.2978 |
0.0496 |
0.0410 |
0.2660 |
363.15 |
156.74 |
0.3995 |
0.0987 |
0.0810 |
0.3400 |
363.15 |
146.85 |
0.4009 |
0.2953 |
0.1660 |
0.4440 |
363.15 |
150.57 |
0.4978 |
0.1504 |
0.1330 |
0.4220 |
363.15 |
151.98 |
0.5045 |
0.1240 |
0.1150 |
0.4070 |
363.15 |
151.38 |
0.7019 |
0.0293 |
0.0720 |
0.4510 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Diethyl carbonate (1) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Diethyl carbonate (1) - Liquid mixture 2 |
Mole fraction of Water (3) - Gas |
Mole fraction of Diethyl carbonate (1) - Gas |
353.15 |
0.75 |
0.6277 |
0.3677 |
0.9862 |
0.0072 |
0.6472 |
0.2344 |
353.15 |
0.82 |
0.5372 |
0.4002 |
0.9661 |
0.0096 |
0.5914 |
0.2011 |
353.15 |
0.80 |
0.4639 |
0.4345 |
0.9607 |
0.0089 |
0.5705 |
0.1859 |
353.15 |
0.82 |
0.3566 |
0.4826 |
0.9396 |
0.0111 |
0.5599 |
0.1766 |
353.15 |
0.82 |
0.2851 |
0.5292 |
0.9255 |
0.0121 |
0.5567 |
0.1733 |
353.15 |
0.87 |
0.1467 |
0.6599 |
0.8854 |
0.0218 |
0.5496 |
0.1637 |
363.15 |
1.25 |
0.5805 |
0.4137 |
0.9862 |
0.0072 |
0.6126 |
0.2683 |
363.15 |
1.27 |
0.5098 |
0.4287 |
0.9756 |
0.0104 |
0.5533 |
0.2333 |
363.15 |
1.22 |
0.4215 |
0.4630 |
0.9661 |
0.0096 |
0.5274 |
0.2176 |
363.15 |
1.22 |
0.2882 |
0.5403 |
0.9607 |
0.0089 |
0.5177 |
0.1999 |
363.15 |
1.22 |
0.2274 |
0.5876 |
0.9396 |
0.0111 |
0.5103 |
0.1897 |
363.15 |
1.14 |
0.1400 |
0.6784 |
0.9255 |
0.0121 |
0.4981 |
0.1788 |
Temperature, K x Mole fraction
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Mole fraction of Water (3) - Liquid mixture 1 |
Mole fraction of Diethyl carbonate (1) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Diethyl carbonate (1) - Liquid mixture 2 |
296.15 |
0.9415 |
0.0107 |
0.2439 |
0.7330 |
333.15 |
0.8492 |
0.0212 |
0.4804 |
0.2732 |
333.15 |
0.8163 |
0.0264 |
0.5753 |
0.1777 |
318.15 |
0.9089 |
0.0129 |
0.3137 |
0.5537 |
333.15 |
0.9607 |
0.0093 |
0.2833 |
0.6720 |
333.15 |
0.9918 |
0.0082 |
0.2464 |
0.7536 |
333.15 |
0.9217 |
0.0121 |
0.3380 |
0.5210 |
303.15 |
0.9003 |
0.0121 |
0.2879 |
0.5946 |
338.15 |
0.9000 |
0.0151 |
0.4046 |
0.4035 |
338.15 |
0.8088 |
0.0358 |
0.5967 |
0.1676 |
338.15 |
0.8685 |
0.0183 |
0.4624 |
0.3076 |
323.15 |
0.9133 |
0.0133 |
0.3218 |
0.5409 |
338.15 |
0.9600 |
0.0105 |
0.2968 |
0.6573 |
296.15 |
0.7912 |
0.0276 |
0.4488 |
0.2710 |
338.15 |
0.9254 |
0.0121 |
0.3468 |
0.5201 |
318.15 |
0.8883 |
0.0146 |
0.3718 |
0.4345 |
296.15 |
0.9925 |
0.0075 |
0.2134 |
0.7866 |
296.15 |
0.8976 |
0.0111 |
0.2697 |
0.6243 |
296.15 |
0.8688 |
0.0117 |
0.3090 |
0.5221 |
303.15 |
0.8507 |
0.0162 |
0.3632 |
0.4161 |
303.15 |
0.7983 |
0.0283 |
0.4686 |
0.2603 |
303.15 |
0.8292 |
0.0197 |
0.4049 |
0.3448 |
323.15 |
0.8840 |
0.0142 |
0.3743 |
0.4270 |
303.15 |
0.9904 |
0.0096 |
0.2241 |
0.7759 |
303.15 |
0.8724 |
0.0141 |
0.3244 |
0.4958 |
318.15 |
0.8383 |
0.0205 |
0.4549 |
0.2951 |
318.15 |
0.8582 |
0.0174 |
0.4181 |
0.3513 |
296.15 |
0.8426 |
0.0161 |
0.3442 |
0.4363 |
318.15 |
0.9511 |
0.0103 |
0.2771 |
0.6814 |
318.15 |
0.8014 |
0.0319 |
0.5296 |
0.2114 |
318.15 |
0.9913 |
0.0087 |
0.2426 |
0.7574 |
323.15 |
0.8400 |
0.0216 |
0.4724 |
0.2786 |
323.15 |
0.8608 |
0.0175 |
0.4333 |
0.3374 |
303.15 |
0.9461 |
0.0098 |
0.2556 |
0.7161 |
323.15 |
0.9524 |
0.0098 |
0.2818 |
0.6723 |
323.15 |
0.8052 |
0.0313 |
0.5468 |
0.1981 |
323.15 |
0.9917 |
0.0083 |
0.2578 |
0.7422 |
333.15 |
0.8689 |
0.0176 |
0.4332 |
0.3351 |
296.15 |
0.8223 |
0.0197 |
0.3828 |
0.3652 |
333.15 |
0.8962 |
0.0147 |
0.3770 |
0.4342 |
Mole fraction
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid mixture 2)
- Temperature, K = 303.15 (Liquid mixture 2)
Fixed |
Measured |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Ethanol (2) - Liquid mixture 2 |
Mole fraction of Ethanol (2) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 1 |
0.9990 |
0.0000 |
0.0000 |
0.0530 |
0.9770 |
0.0200 |
0.0230 |
0.0610 |
0.9510 |
0.0450 |
0.0590 |
0.0820 |
0.9290 |
0.0670 |
0.0960 |
0.1110 |
0.9040 |
0.0900 |
0.1450 |
0.1470 |
0.8860 |
0.1070 |
0.1870 |
0.1870 |
0.8630 |
0.1260 |
0.2270 |
0.2480 |
0.8420 |
0.1430 |
0.2570 |
0.3110 |
0.8220 |
0.1570 |
0.2710 |
0.3780 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Water (3) - Liquid |
Mole fraction of Diethyl carbonate (1) - Liquid |
Mole fraction of Diethyl carbonate (1) - Gas |
Mole fraction of Water (3) - Gas |
353.15 |
61.78 |
0.0469 |
0.9037 |
0.3572 |
0.4134 |
353.15 |
94.30 |
0.0484 |
0.5032 |
0.1633 |
0.1379 |
353.15 |
109.49 |
0.0488 |
0.0491 |
0.0318 |
0.0757 |
353.15 |
93.14 |
0.0976 |
0.6531 |
0.2068 |
0.3065 |
353.15 |
103.76 |
0.0989 |
0.2994 |
0.1180 |
0.1688 |
353.15 |
108.91 |
0.1179 |
0.1521 |
0.0755 |
0.1626 |
353.15 |
103.54 |
0.2056 |
0.3962 |
0.1465 |
0.3367 |
353.15 |
94.72 |
0.2183 |
0.6704 |
0.2198 |
0.5470 |
353.15 |
100.45 |
0.2481 |
0.5005 |
0.1756 |
0.4440 |
353.15 |
107.16 |
0.2518 |
0.2491 |
0.1132 |
0.3160 |
353.15 |
112.94 |
0.3095 |
0.0489 |
0.0394 |
0.2750 |
353.15 |
109.89 |
0.3981 |
0.0986 |
0.0757 |
0.3531 |
353.15 |
101.47 |
0.4010 |
0.3021 |
0.1507 |
0.4540 |
353.15 |
104.76 |
0.5022 |
0.1504 |
0.1175 |
0.4249 |
353.15 |
106.01 |
0.5052 |
0.1250 |
0.1038 |
0.4193 |
353.15 |
105.10 |
0.7015 |
0.0295 |
0.0718 |
0.4366 |
363.15 |
87.85 |
0.0465 |
0.9058 |
0.3710 |
0.4040 |
363.15 |
134.63 |
0.0483 |
0.5042 |
0.1880 |
0.1250 |
363.15 |
156.65 |
0.0491 |
0.0492 |
0.0350 |
0.0730 |
363.15 |
131.90 |
0.0973 |
0.6537 |
0.2200 |
0.2990 |
363.15 |
147.90 |
0.1012 |
0.2983 |
0.1340 |
0.1820 |
363.15 |
155.27 |
0.1190 |
0.1460 |
0.0840 |
0.1520 |
363.15 |
147.72 |
0.2019 |
0.3928 |
0.1660 |
0.3110 |
363.15 |
134.19 |
0.2122 |
0.6756 |
0.2340 |
0.5300 |
363.15 |
143.65 |
0.2471 |
0.5006 |
0.2060 |
0.4200 |
363.15 |
152.97 |
0.2508 |
0.2490 |
0.1320 |
0.3030 |
363.15 |
160.62 |
0.2978 |
0.0496 |
0.0410 |
0.2660 |
363.15 |
156.74 |
0.3995 |
0.0987 |
0.0810 |
0.3400 |
363.15 |
146.85 |
0.4009 |
0.2953 |
0.1660 |
0.4440 |
363.15 |
150.57 |
0.4978 |
0.1504 |
0.1330 |
0.4220 |
363.15 |
151.98 |
0.5045 |
0.1240 |
0.1150 |
0.4070 |
363.15 |
151.38 |
0.7019 |
0.0293 |
0.0720 |
0.4510 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mole fraction of Diethyl carbonate (1) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Diethyl carbonate (1) - Liquid mixture 2 |
Mole fraction of Water (3) - Gas |
Mole fraction of Diethyl carbonate (1) - Gas |
353.15 |
0.75 |
0.6277 |
0.3677 |
0.9862 |
0.0072 |
0.6472 |
0.2344 |
353.15 |
0.82 |
0.5372 |
0.4002 |
0.9661 |
0.0096 |
0.5914 |
0.2011 |
353.15 |
0.80 |
0.4639 |
0.4345 |
0.9607 |
0.0089 |
0.5705 |
0.1859 |
353.15 |
0.82 |
0.3566 |
0.4826 |
0.9396 |
0.0111 |
0.5599 |
0.1766 |
353.15 |
0.82 |
0.2851 |
0.5292 |
0.9255 |
0.0121 |
0.5567 |
0.1733 |
353.15 |
0.87 |
0.1467 |
0.6599 |
0.8854 |
0.0218 |
0.5496 |
0.1637 |
363.15 |
1.25 |
0.5805 |
0.4137 |
0.9862 |
0.0072 |
0.6126 |
0.2683 |
363.15 |
1.27 |
0.5098 |
0.4287 |
0.9756 |
0.0104 |
0.5533 |
0.2333 |
363.15 |
1.22 |
0.4215 |
0.4630 |
0.9661 |
0.0096 |
0.5274 |
0.2176 |
363.15 |
1.22 |
0.2882 |
0.5403 |
0.9607 |
0.0089 |
0.5177 |
0.1999 |
363.15 |
1.22 |
0.2274 |
0.5876 |
0.9396 |
0.0111 |
0.5103 |
0.1897 |
363.15 |
1.14 |
0.1400 |
0.6784 |
0.9255 |
0.0121 |
0.4981 |
0.1788 |
Temperature, K x Mole fraction
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Mole fraction of Water (3) - Liquid mixture 1 |
Mole fraction of Diethyl carbonate (1) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Diethyl carbonate (1) - Liquid mixture 2 |
296.15 |
0.9415 |
0.0107 |
0.2439 |
0.7330 |
333.15 |
0.8492 |
0.0212 |
0.4804 |
0.2732 |
333.15 |
0.8163 |
0.0264 |
0.5753 |
0.1777 |
318.15 |
0.9089 |
0.0129 |
0.3137 |
0.5537 |
333.15 |
0.9607 |
0.0093 |
0.2833 |
0.6720 |
333.15 |
0.9918 |
0.0082 |
0.2464 |
0.7536 |
333.15 |
0.9217 |
0.0121 |
0.3380 |
0.5210 |
303.15 |
0.9003 |
0.0121 |
0.2879 |
0.5946 |
338.15 |
0.9000 |
0.0151 |
0.4046 |
0.4035 |
338.15 |
0.8088 |
0.0358 |
0.5967 |
0.1676 |
338.15 |
0.8685 |
0.0183 |
0.4624 |
0.3076 |
323.15 |
0.9133 |
0.0133 |
0.3218 |
0.5409 |
338.15 |
0.9600 |
0.0105 |
0.2968 |
0.6573 |
296.15 |
0.7912 |
0.0276 |
0.4488 |
0.2710 |
338.15 |
0.9254 |
0.0121 |
0.3468 |
0.5201 |
318.15 |
0.8883 |
0.0146 |
0.3718 |
0.4345 |
296.15 |
0.9925 |
0.0075 |
0.2134 |
0.7866 |
296.15 |
0.8976 |
0.0111 |
0.2697 |
0.6243 |
296.15 |
0.8688 |
0.0117 |
0.3090 |
0.5221 |
303.15 |
0.8507 |
0.0162 |
0.3632 |
0.4161 |
303.15 |
0.7983 |
0.0283 |
0.4686 |
0.2603 |
303.15 |
0.8292 |
0.0197 |
0.4049 |
0.3448 |
323.15 |
0.8840 |
0.0142 |
0.3743 |
0.4270 |
303.15 |
0.9904 |
0.0096 |
0.2241 |
0.7759 |
303.15 |
0.8724 |
0.0141 |
0.3244 |
0.4958 |
318.15 |
0.8383 |
0.0205 |
0.4549 |
0.2951 |
318.15 |
0.8582 |
0.0174 |
0.4181 |
0.3513 |
296.15 |
0.8426 |
0.0161 |
0.3442 |
0.4363 |
318.15 |
0.9511 |
0.0103 |
0.2771 |
0.6814 |
318.15 |
0.8014 |
0.0319 |
0.5296 |
0.2114 |
318.15 |
0.9913 |
0.0087 |
0.2426 |
0.7574 |
323.15 |
0.8400 |
0.0216 |
0.4724 |
0.2786 |
323.15 |
0.8608 |
0.0175 |
0.4333 |
0.3374 |
303.15 |
0.9461 |
0.0098 |
0.2556 |
0.7161 |
323.15 |
0.9524 |
0.0098 |
0.2818 |
0.6723 |
323.15 |
0.8052 |
0.0313 |
0.5468 |
0.1981 |
323.15 |
0.9917 |
0.0083 |
0.2578 |
0.7422 |
333.15 |
0.8689 |
0.0176 |
0.4332 |
0.3351 |
296.15 |
0.8223 |
0.0197 |
0.3828 |
0.3652 |
333.15 |
0.8962 |
0.0147 |
0.3770 |
0.4342 |
Mole fraction
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid mixture 2)
- Temperature, K = 303.15 (Liquid mixture 2)
Fixed |
Measured |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Ethanol (2) - Liquid mixture 2 |
Mole fraction of Ethanol (2) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 1 |
0.9990 |
0.0000 |
0.0000 |
0.0530 |
0.9770 |
0.0200 |
0.0230 |
0.0610 |
0.9510 |
0.0450 |
0.0590 |
0.0820 |
0.9290 |
0.0670 |
0.0960 |
0.1110 |
0.9040 |
0.0900 |
0.1450 |
0.1470 |
0.8860 |
0.1070 |
0.1870 |
0.1870 |
0.8630 |
0.1260 |
0.2270 |
0.2480 |
0.8420 |
0.1430 |
0.2570 |
0.3110 |
0.8220 |
0.1570 |
0.2710 |
0.3780 |
Sources